Increasing ionic conductivity of lithium titanium thiophosphate by sintering

ABSTRACT

A method of treatment of a sample of lithium titanium thiophosphate LiTi 2 (PS 4 ) 3  including: (a) providing a solid sample of lithium titanium thiophosphate LiTi 2 (PS 4 ) 3 , (b) compressing the lithium titanium thiophosphate sample provided in step (a) to form a compressed powder layer; and (c) sintering the lithium titanium thiophosphate obtained as a compressed powder layer in step (b) at a temperature of at least 200° C. and at most 400° C.

FIELD OF THE INVENTION

The present invention relates to a method of increasing the ionic conductivity of lithium titanium thiophosphate LiTi₂(PS₄)₃ through a sintering process.

BACKGROUND ART

The all-solid-state battery system offers the possibility of high energy density of the battery pack. In order to realize such systems, a solid electrolyte which exhibits high ionic conductivity is demanded. LiTi₂(PS₄)₃ is a candidate for such a solid electrolyte, and has been described in Kim et al., Chem. Mater. 2008, 20, 470-474; Kim et al., Electrochemistry Communications 10 (2008) 497-501; and Shin et al., Journal of The Electrochemical Society, 161 (1) A154-A159 (2014).

According to the method of synthesis described in Kim et al., Chem. Mater. 2008, 20, 470-474, a stoichiometric mixture of Li₂S, TiS₂ and P₂S₅ is mixed and heated under vacuum according to the following temperature profile:

However, the method of preparation proposed in the literature was not optimized with respect to ionic conductivity.

SUMMARY OF THE INVENTION

With a view to solving the above-referenced problems in the preparation of lithium titanium thiophosphate LiTi₂(PS₄)₃, the present inventor has studied different aspects of the preparation of this material, and this work has led to the achievement of the present invention.

In one aspect, the present invention is thus directed to a method of treatment of a sample of lithium titanium thiophosphate LiTi₂(PS₄)₃ comprising the steps of:

(a) providing a solid sample of lithium titanium thiophosphate LiTi₂(PS₄)₃;

(b) compressing the lithium titanium thiophosphate sample provided in step (a) to form a compressed powder layer; and

(c) sintering the lithium titanium thiophosphate obtained as a compressed powder layer in step (b) at a temperature of at least 200° C. and at most 400° C.

The method of treatment of a sample of lithium titanium thiophosphate according to the invention has been found by the inventor to enable higher ionic conductivity to be obtained for this type of material.

In another aspect, the present invention relates to a complete preparation process of lithium titanium thiophosphate LiTi₂(PS₄)₃ starting from the simple (not mixed) sulfides of Li, Ti and P, in an overall process designed by the present inventor to minimize levels of impurity and maximize ionic conductivity. Thus, in this aspect, the invention is concerned with a method of preparation of lithium titanium thiophosphate LiTi₂(PS₄)₃ comprising the steps of:

(α) providing a mixture of lithium sulfide Li₂S, phosphorus sulfide P₂S₅ and titanium sulfide TiS₂;

(β) subjecting the mixture prepared in step (α) to a preliminary reaction step through mechanical milling or melt-quenching to produce an intermediate amorphous sulfide mixture;

(γ) subjecting the mixture prepared in step (β) to a heat treatment step at a maximum plateau temperature of at least 350° C. and less than 500° C.; wherein the material obtained through step (γ) is subsequently subjected to the method of treatment of a sample of lithium titanium thiophosphate LiTi₂(PS₄)₃ comprising the steps (a), (b) and (c) as set out above.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows X-ray diffraction patterns (XRD) of lithium titanium thiophosphate LiTi₂(PS₄)₃ samples obtained according to the process of the present invention (embodiments illustrated in a non-limiting manner by Examples 1 to 4) or according to other processes not according to the present invention (Comparative Examples 1 and 2).

FIG. 2 shows results obtained in certain Examples and Comparative Examples of the present invention and in particular the observed effect of sintering temperature on ionic conductivity.

FIG. 3 shows schematically an illustrative and non-limiting embodiment of the present invention including steps of synthesis of the LiTi₂(PS₄)₃ prior to the use of sintering steps according to the present invention.

DETAILED DESCRIPTION OF THE INVENTION

Without wishing to be bound by any particular theory, it is believed that the low ionic conductivity of LiTi₂(PS₄)₃ obtained according to literature methods may be due at least in part to large grain boundary resistance. To solve this problem, this invention provides an additional sintering process. The sintering process is believed to promote diffusion of elements at the grain boundary, to lead to improved connection of the polycrystals at the grain boundary, and thereby to cause a decrease in resistance.

From the results obtained by the present inventor, the sintering temperature T range of 200° C.≤T≤400° C. is observed to be preferable to obtain high ionic conductivity of LiTi₂(PS₄)₃. A more preferred range is a temperature of at least 250° C. and at most 375° C. Particularly preferred sintering temperature ranges are from at least 275° C. to at most 375° C.

In the method of treatment of a sample of lithium titanium thiophosphate according to the invention, in step (b), the sample of lithium titanium thiophosphate may preferably be compressed at a pressure range of at least 100 MPa and at most 1500 MPa. The compression step (b) may give rise to samples in pellet form, but the size of the pellets is not important in producing the final effect of increased ionic conductivity.

In the method of treatment of a sample of lithium titanium thiophosphate according to the invention, in step (c), the sintering time is at least 1 hour and at most 300 hours. Here, by “sintering time” reference is made to the plateau temperature maintained in a heating programme. Concerning the temperature vs. time heating profile appropriate before and after reaching the sintering plateau temperature, a generally appropriate heating rate is 0.1° C. min⁻¹ to 20° C. min⁻¹. After the sintering time appropriately of 1 hour to 300 hours at the sintering temperature of 200° C.≤T≤400° C., cooling can be carried out by natural cooling or controlled cooling. If the cooling process is controlled, the cooling rate may appropriately be 0.1° C. min⁻¹ to 100° C. min⁻¹.

In the present invention, lithium titanium thiophosphate LiTi₂(PS₄)₃ samples prepared according to known methods can be treated by the process of the invention, notably with a view to increasing ionic conductivity.

In a preferred embodiment, the present invention uses, as starting materials for compression into a pellet and sintering, lithium titanium thiophosphate LiTi₂(PS₄)₃ samples obtained by a method of synthesis comprising the steps of:

(α) providing a mixture of lithium sulfide Li₂S, phosphorus sulfide P₂S₅ and titanium sulfide TiS₂;

(β) subjecting the mixture prepared in step (α) to a preliminary reaction step through mechanical milling or melt-quenching to produce an intermediate amorphous sulfide mixture;

(γ) subjecting the mixture prepared in step (β) to a heat treatment step at a maximum plateau temperature of at least 350° C. and less than 500° C.;

Here “maximum plateau temperature” refers to the maximum temperature maintained in a heating vessel as commonly used in solid state chemistry, the temperature vs. time profile typically including a gradual ascent phase with a controlled rate of increase of temperature starting from room temperature, a chosen reaction temperature maintained effectively constant over a period of time (the “maximum plateau temperature”), and then a descent phase wherein the temperature is brought back down to room temperature.

According to the above preferred method of synthesis of LiTi₂(PS₄)₃ starting from the sulfides of Li, Ti and P, an intermediate step is used consisting of subjecting the mixture of starting materials to a preliminary reaction step through mechanical milling or melt-quenching to produce an intermediate amorphous sulfide mixture. This intermediate step may also be referred to hereinafter as an “amorphasizing step”, and provides amorphous materials derived from Li₂S—TiS₂—P₂S₅. This amorphous material is able to be heat-treated at over 400° C. without melting. Without the intermediate step, the specimens are melted due to the low melting point of P₂S₅ (˜270° C.) Elemental phosphorus and sulfur also have lower melting points and will thus melt before the temperatures needed to produce LiTi₂(PS₄)₃ product in the solid phase reaction. It is considered that the most important effect of the intermediate step is allowing Li₂S, TiS₂ and P₂S₅ to completely mix and react with each other—the intermediate step may, as well as ensuring intimate physical mixing, begin the chemical transformations which will lead to the final product. The intermediate step may thus act to react the low melting material of P₂S₅ with Li₂S (or at least start this reaction).

In terms of starting material mole ratios, the method is appropriately carried out with as close as possible to a stoichiometric ratio thereof in view of the final product LiTi₂(PS₄)₃ product to be produced. Thus, the lithium sulfide Li₂S, phosphorus sulfide P₂S₅ and titanium sulfide TiS₂ starting materials are generally used in a Li₂S:P₂S₅:TiS₂ mole ratio of 1:3:4.

The amorphous material obtained through the “amorphasizing step” can advantageously be heat-treated at the temperature of 300° C.≤T<500° C. More generally, in heat treatment step (γ), the maximum plateau temperature is appropriately not more than 475° C., and preferably at least 375° C., more preferably at least 400° C. and at most 450° C. Further, in heat treatment step (γ), the maximum plateau temperature during heat treatment is appropriately maintained for at least 1 hour and at most 300 hours. In terms of the speed of temperature increase going from room temperature up to the maximum plateau temperature, before the heat treatment step, a generally appropriate range is from 0.1° C. min⁻¹ to 20° C. min⁻¹. A preferred speed is in the range of 1° C. min⁻¹ to 5° C. min⁻¹. Analogous rates of temperature decrease after the heat treatment step, may also be used to bring the sample back down to room temperature.

In the method of synthesis of LiTi₂(PS₄)₃ used in preferred embodiments of the present invention, each of the method steps (α), (β) and (γ) is advantageously carried out under an inert gas, for example, nitrogen or argon, preferably argon.

As mentioned above, the intermediate step (β), also referred to herein as an “amorphasizing step”, the intermediate step giving rise to an intermediate amorphous sulfide mixture, may be a carried out by a “melt-quenching” procedure. In an appropriate melt-quenching step, the starting materials are heated to a temperature higher than the melting point of the final product LiTi₂(PS₄)₃, i.e. to over 700° C. However, in most cases, it is preferable for a sample to be in the equilibrium state before quenching. Therefore, it is appropriate to wait for a relatively longer period and heat up more slowly, for example with a heating rate of 0.05° C. min⁻¹ to 20° C. min′, with a holding time of appropriately 3 hours to 300 hours. To quench the molten mixture, raised to a temperature above 700° C., a rapid cooling rate is used, appropriately between 300 to 1000 K s⁻¹, to bring the mixture to room temperature of below. A generally appropriate method for sulfide amorphous materials is ice quenching. A heated quartz tube containing the material to be quenched is placed in ice water.

In preferred embodiments for carrying out the present invention, the intermediate step (β), also referred to herein as an “amorphasizing step”, the intermediate step giving rise to an intermediate amorphous sulfide mixture, is carried out by a mechanical milling procedure, such as planetary ball milling, vibration milling or jet milling. Where the preferred method of planetary ball milling is used, a generally appropriate ball size range is chosen within the range 1 mm≤ϕ≤10 mm), the temperature range is chosen within the range 0° C. T 60° C., the rotation speed is chosen within the range 200 rpm≤R≤500 rpm, and the duration is chosen within the range 5 h≤t≤200 h.

In a further aspect, the present disclosure relates to an all-solid-state lithium battery comprising the following elements:

-   -   a positive electrode active material layer;     -   a solid electrolyte layer;     -   a negative electrode active material layer,         wherein the solid electrolyte layer contains a lithium titanium         thiophosphate LiTi₂(PS₄)₃ material produced according to the         present invention, and is positioned between the positive         electrode active material layer and negative electrode active         material layer.

In such an all-solid-state lithium battery, using as solid electrolyte, the LiTi₂(PS₄)₃ sulfide materials produced according to the present invention, concerning the form of the solid electrolyte materials, examples include a particle shape, such as the shape of a true ball and the shape of an elliptical ball, or a thin film form, for example. When solid electrolyte materials have a particle shape, as for the mean particle diameter, it is preferable that their size is within the range of 50 nm to 10 micrometers, more preferably within the range of 100 nm to 5 micrometers.

Although it is preferable to have only one or more solid electrolyte materials as mentioned above in a solid electrolyte layer, this layer may also contain a binding agent if needed. As a binding agent used for a solid electrolyte layer, this may be of the same type as mentioned hereunder for the positive active material layer.

As regards the thickness of a solid electrolyte layer, although this may change with the kind of solid electrolyte materials, and the overall composition of an all-solid battery, generally it is preferable that this thickness is within the range of 0.1 micrometer to 1000 micrometers, more preferably within the range of 0.1 micrometer to 300 micrometers.

Concerning the positive active material (cathode active material) to be used in the positive electrode (cathode) active material layer, this is not especially limited if the average operating potential becomes more than 4 V (vs. Li/Li⁺). As an average operating potential of positive active material, this is appropriately more than 4 V (vs. Li/Li⁺), and it is preferable that it is within the limits of 4.0 V to 6.0 V, still more preferably within the limits of 4.5 V to 5.5 V. The average operating potential can be evaluated using cyclic voltammetry, for example. In particular, when cyclic voltammetry is measured at a small electric potential speed like 0.1 mV/sec, it can be considered that the average value of the voltage which gives the peak current on the side of oxidation, and the voltage which gives the peak current on the side of reduction is the average operating potential.

As a positive active material, especially if the average operating potential is made with more than 4 V (vs. Li/Li⁺), there is no specific limitation, but it is preferable that the material is an oxide positive active material, which can have a high energy density.

A compound which has the spinel type structure denoted by general formula LiM₂O₄ (M is at least one kind of transition metal element), as an example of positive active material, can be mentioned as an example. As regards M of the above-mentioned general formula LiM₂O₄, especially if it is a transition metal element, it will not be limited, but it is preferable that it is at least one kind chosen from the group which consists of Ni, Mn, Cr, Co, V, and Ti, for example, and it is more preferable that it is at least one kind chosen from the group which consists of Ni, Mn, and Cr especially. Specifically, LiCr_(0.05)Ni_(0.50)Mn_(1.45)O₄, LiCrMnO₄, LiNi_(0.5)Mn_(1.5)O₄, etc. can be mentioned. The compound which has the olivine type structure denoted by general formula LiMPO₄ (M is at least one kind of transition metal element) as other examples of positive active material can be mentioned. M in the above-mentioned general formula will not be limited especially if it is a transition metal element, but it is preferable that it is at least one kind chosen from Mn, Co, Ni, and the group that consists of V, for example, and it is more preferable that it is at least one kind chosen from the group which consists of Mn, Co, and Ni especially. Specifically, LiMnPO₄, LiCoPO₄, LiNiPO₄, etc. can be mentioned. The compound which has the layer structure denoted by general formula LiMO₂ (M is at least 1 type of a transition metal element) as other examples of positive active material can be mentioned. Specifically, LiCoO₂, LiNi_(0.5)Mn_(0.5)O₂ and LiNi_(0.33)Co_(0.33)Mn_(0.33)O₂ etc. can be mentioned. As examples other than the positive active material mentioned above, a Li₂MnO₃—LiNi_(1/3)Co_(1/3)Mn_(1/3)O₂ solid solution, a Li₂MnO₃—LiNi_(0.5)Mn_(1.5)O₂ solid solution, a Li₂MnO₃—LiFeO₂ solid solution, etc. can be mentioned.

As regards the form of the positive active material, a particle shape, such as the shape of a true ball and the shape of an elliptical ball, thin film form, etc. can be mentioned, as an example. As for the mean particle diameter, when the positive active material has a particle shape, it is preferable that it is within the size range of 0.1 micrometer to 50 micrometers, for example. As for the content of the positive active material in a positive active material layer, it is preferable that it is in the range of 10% by weight to 99% by weight, for example, more preferably from 20% by weight to 90% by weight.

Concerning the positive active material layer, in addition to the positive active material mentioned above, if needed, the positive active material layer in may contain other materials, for example, solid electrolyte materials etc. As for the content of the solid electrolyte materials in a positive active material layer, it is preferable that this content is 1% by weight to 90% by weight, more preferably 10% by weight to 80% by weight.

Furthermore, a positive active material layer may contain an electrically conductive agent from a viewpoint of improving the conductivity of a positive active material layer, other than the solid electrolyte materials mentioned above. As electrically conductive material, acetylene black, Ketjenblack, a carbon fiber, etc. can be mentioned, for example. A positive active material may also contain a binding agent. As such a binding material (binding agent), fluorine-based binding materials, such as polyvinylidene fluoride (PVDF) and polytetrafluoroethylene (PTFE), etc. can be mentioned, for example.

Although the thickness of a positive active material layer may change according to the kind of all-solid-state battery made, it is generally preferable that it is within the range of 0.1 micrometer to 1000 micrometers.

As regards the negative electrode active material layer, this layer at least contains one or more negative electrode active material(s), and may additionally contain at least one or more of solid electrolyte materials and electrically conductive agents if needed. For all-solid-state lithium batteries, the negative electrode active material is not limited provided that occlusion and discharge of the Li ion, which is a conduction ion, are possible. As a negative electrode active material, a carbon active material, a metal active material, etc. can be mentioned, for example. As a carbon active material, black lead, meso carbon micro beads (MCMB), highly ordered/oriented pyrolytic graphite (HOPG), hard carbon, soft carbon, etc. can be mentioned as examples. On the other hand, as a metal active material, charges of an alloy, such as Li alloy and Sn—Co—C, In, Al, Si, Sn, etc. can be mentioned as examples. Oxide stock materials, such as Li₄Ti₅O₁₂, can be mentioned as examples of other negative electrode active materials.

Concerning solid electrolyte materials used for the negative electrode active material layer, and an electrically conductive agent, these may be the same as that for the solid electrolyte layer and positive active material layer mentioned above.

The thickness of the negative electrode active material layer will generally be appropriately within the range of 0.1 micrometer to 1000 micrometers.

An all-solid-state battery of the present disclosure has at least the positive active material layer, solid electrolyte layer, and negative electrode active material layer which were mentioned above. It further usually has a positive pole collector which collects a positive active material layer, and a negative pole collector which performs current collection of a negative electrode active material layer. As a material of a positive pole collector, for example, SUS (stainless steel), aluminum, nickel, iron, titanium, carbon, etc. can be mentioned, and SUS is especially preferable. On the other hand as a material of a negative pole collector, SUS, copper, nickel, carbon, etc. can be mentioned, for example, and SUS is especially preferable. Concerning the thickness, form, etc. of a positive pole collector and a negative pole collector, the person skilled in the art may choose suitably according to the use of the all-solid-state battery, etc. The cell case used for a common all-solid-state battery can be used, for example, the cell case made from SUS, etc. can be mentioned. The all-solid-state battery may form a power generation element in the inside of an insulating ring.

The all-solid-state battery of the present disclosure can be considered as a chargeable and dischargeable all-solid-state battery in a room temperature environment. Although it may be a primary battery and may be a rechargeable battery, it is especially preferable that it is a rechargeable battery. Concerning the form of the all-solid-state battery, a coin type, a laminated type, cylindrical, a square shape, etc. can be mentioned, as examples.

As regards the manufacturing method of the all-solid-state battery, this is not particularly limited, and common manufacturing methods of all-solid-state batteries can be used. For example, when an all-solid-state battery is in the thin film form, a positive active material layer can be formed on a substrate, and the method of forming a solid electrolyte layer and a negative electrode active material layer in order, and laminating them thereafter etc., may be used.

Within the practice of the present invention, it may be envisaged to combine any features or embodiments which have hereinabove been separately set out and indicated to be advantageous, preferable, appropriate or otherwise generally applicable in the practice of the invention. The present description should be considered to include all such combinations of features or embodiments described herein unless such combinations are said herein to be mutually exclusive or are clearly understood in context to be mutually exclusive.

EXPERIMENTAL SECTION—EXAMPLE

The following experimental section illustrates experimentally the practice of the present invention, but the scope of the invention is not to be considered to be limited to the specific examples that follow.

Example 1

Providing a Solid Sample of Lithium Titanium Thiophosphate LiTi₂(PS₄)₃

For the following experiments, LiTi₂(PS₄)₃ was synthesized using starting materials Li₂S (Sigma), TiS₂ (Sigma), and P₂S₅ (Aldrich). In a first mixing step, these starting material sulfides were mixed at the weight ratio listed in Table 1 below:

TABLE 1 Weight ratio of starting materials for LiTi₂(PS₄)₃ synthesis Weight of starting material (g) mmol of starting material Li₂S 0.039584 0.8615 P₂S₅ 0.57447 2.5845 TiS₂ 0.385946 3.4460

In a subsequent amorphasizing step, the mixed sample thus obtained was put into a zirconium pot (45 mL) with 18 zirconium balls (ϕ10 mm) under argon. The pot was closed and treated with planetary milling equipment (Fritsch, P7) at 370 rpm for 40 h to obtain the precursor.

Following the amorphasizing step, in a heat treatment step, the precursor was sealed into a glass tube at a pressure of 30 Pa and then heated at T=400° C. for 8 h. A heating rate of 2.2° C. min⁻¹ was used to bring the sample from room temperature up to the heat treatment temperature. At the heat treatment temperature of 400° C., the sample was not melted.

The lithium titanium thiophosphate LiTi₂(PS₄)₃ obtained after this heat treatment process is in powder form. The powder is colored dark green. The particle size is approximately distributed from 100 μm to 10 μm.

Compression of Lithium Titanium Thiophosphate Sample

100 mg of the sulfide solid electrolyte material LiTi₂(PS₄)₃ in powder form obtained by the heat treatment process described above was added to a cylinder made of alumina and pressed at 4 ton/cm² to form a solid electrolyte layer in the form of a pellet.

Sintering Step

The pellet was again sealed into the glass tube at a pressure of 30 Pa and then heated at T=200° C. In terms of temperature vs. time heating profile, before and after reaching the sintering temperature, the temperature of the oven was increased at the heating rate of 2.2° C. min⁻¹, and then held for 8 hours. After that the oven was turned off, and the sample was cooled down to room temperature in 5 hours.

Measurement of Li Ion Conductance

The pellet, after the sintering step above, was sandwiched by SUS current collector for measuring impedance spectroscopy.

An impedance gain-phase analyzer manufactured by Biologic (VMP3) was used for the measurement as FRA (Frequency Response Analyzer). The measurement was started from a high-frequency range with the conditions of an alternating voltage of 5 mV and a frequency range of 1 Hz to 1 MHz.

Li ion conductance was measured at a temperature of 25° C.

The ionic conductivity of the material prepared in Example 1 was 7.5×10⁻⁵ S/cm.

X-Ray Diffraction Measurement

X-ray diffraction measurement (using a CuKα line) was performed by using the sulfide solid electrolyte materials obtained in Examples and in Comparative Examples. The results are shown in FIG. 1. Essentially only the peak of LiTi₂(PS₄)₃ was detected.

Example 2

Only the sintering temperature T was different from Example 1. Here, a sintering temperature of T=300° C. was used.

The ionic conductivity of Example 2 was 19×10⁻⁵ S/cm.

Essentially only the peak of LiTi₂(PS₄)₃ was detected by XRT.

Example 3

Only the sintering temperature T was different from Example 1. Here, a sintering temperature of T=350° C. was used.

The ionic conductivity of Example 3 was 18×10⁻⁵ S/cm.

Essentially only the peak of LiTi₂(PS₄)₃ was detected by XRT.

Example 4

Only the sintering temperature T was different from Example 1. Here, a sintering temperature of T=400° C. was used.

The ionic conductivity of Example 4 was 12×10⁻⁵ S/cm.

The peaks of LiTi₂(PS₄)₃ and also those of impurity phase were detected by XRT.

Comparative Example 1

Only the sintering temperature T was different from Example 1. Here, a sintering temperature of T=25° C. was used, i.e. no sintering was performed.

The ionic conductivity of Comparative Example 1 was 2.5×10⁻⁵ S/cm.

Essentially only the peak of LiTi₂(PS₄)₃ was detected by XRT.

Comparative Example 2

Only the sintering temperature T was different from Example 1. Here, a sintering temperature of T=600° C. was used.

The ionic conductivity of Comparative Example 2 was 1.0×10⁻⁵ S/cm.

Only peaks due to impurity were detected by XRD.

Temperature Optimization

From the results of Examples and Comparative Examples, the sintering temperature T range of 200° C.≤T≤400° C. is observed to be preferable to obtain high ionic conductivity of LiTi₂(PS₄)₃ (cf. FIG. 2). Without sintering, it is believed that the ionic conductivity was low due to the large grain boundary resistance. When the sintering technique was applied, it is believed that the diffusion between grains was promoted, thereby reducing the grain boundary resistance. For lower sintering temperature, the higher the temperature applied, the higher the ionic conductivity obtained. It is believed that this is because element diffusion was much more promoted by the temperature. However, above 400° C., the conductivity decreased, apparently due to the decomposition of LiTi₂(PS₄)₃ and the generation of impurity phase.

It is generally observed that where lithium titanium thiophosphate LiTi₂(PS₄)₃ was sintered in an optimized temperature range, its ionic conductivity can be increased by a factor of approximately 8 times relative to a non-sintered sample of the same material. 

The invention claimed is:
 1. A method of treatment of a sample of lithium titanium thiophosphate LiTi₂(PS₄)₃ comprising the steps of: (a) providing a solid sample of lithium titanium thiophosphate LiTi₂(PS₄)₃, (b) compressing the lithium titanium thiophosphate sample provided in step (a) to form a compressed powder layer; and (c) sintering the lithium titanium thiophosphate obtained as a compressed powder layer in step (b) at a temperature of at least 200° C. and at most 400° C., wherein in step (b), the sample of lithium titanium thiophosphate is compressed at a pressure range of at least 100 MPa and at most 1500 MPa.
 2. The method of treatment of a sample of lithium titanium thiophosphate according to claim 1, wherein in step (c), the sintering is carried out for a time of at least 1 hour and at most 300 hours.
 3. A method of preparation of lithium titanium thiophosphate LiTi₂(PS₄)₃ comprising the steps of: (α) providing a mixture of lithium sulfide Li₂S, phosphorus sulfide P₂S₅ and titanium sulfide TiS₂; (β) subjecting the mixture prepared in step (α) to a preliminary reaction step through mechanical milling or melt-quenching to produce an intermediate amorphous sulfide mixture; (γ) subjecting the mixture prepared in step (β) to a heat treatment step at a maximum plateau temperature of at least 350° C. and less than 500° C., thereby forming a material; wherein the material obtained through step (γ) is subsequently subjected to the method of claim
 1. 4. The method of preparation of claim 3, wherein the mechanical milling procedure used in step (β) to produce an intermediate amorphous sulfide mixture is planetary ball milling, vibration milling or jet milling.
 5. The method of preparation of claim 3, wherein in the heat treatment step (γ), the maximum plateau temperature is not more than 475° C.
 6. The method of preparation of claim 4, wherein in the heat treatment step (γ), the maximum plateau temperature is not more than 475° C. 